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聚乙烯醇微球预涂动态膜的制备及表征 被引量:1

Preparation and Characterization of Polyvinyl Alcohol Microsphere Pre-coated Dynamic Membranes
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摘要 为了提高微滤膜的抗污染性和降低膜组件的价格,利用循环预涂工艺制备出新型聚乙烯醇微球预涂动态膜(PVA-MS/PCDMs).对不同聚乙烯醇微球预涂量的动态膜进行了系统表征,结果显示,PVA-MS/PCDMs的清水过滤阻力介于0.64×1010~3.84×1010m-1,渗透性良好;当预涂量≥23.9g.m-2时,可达到微滤分离水平;亲水性随预涂量的增加而增强,动态接触角由基膜的118.25°降低到预涂量为61.9g.m-2时的61.52°;利用流动电位法在20℃,pH为8.0±0.2,0.01mol·L-1KCl溶液的测试条件下,测得当预涂量为15.7g.m-2时膜面相对Zeta电位值可达-36.4mV.并且,通过PVA-MS/PCDMs在SMBR中的短期通量衰减变化(恒压)和对EPS的扩散实验发现,预涂量为23.9~61.9g.m-2时,增加了对EPS的扩散渗透性能,且膜通量衰减趋于稳定时仍为基膜的3.5~4.8倍,即提高了抗污染性. To alleviate membrane fouling and reduce the price of membrane module, polyvinyl alcohol mierosphere pre-coated dynamic membranes (PVA-MS/PCDMs) were investigated detailedly. It was prepared when the polyvinyl alcohol mierosphere of the pre-coated reagent deposited on the surface and entered the pores of porous substrate common filter cloth which was low-cost by means of circulatory filtration. The morphology and structure of PVA-MS/PCDMs were examined using scanning electron microscope (SEM), and approximate maximal separated aperture, water eontact angle, pure water permeation resistance and relative Zeta potential of the membrance surface were also determined. The results showed that pure water permeation resistance of PVA-MS/PCDMs was between 0.64 ×10^10m^-1 and 3.84×10^10m^-1 and the approximate maximal separated aperture reached microfiltration level. The hydrophilicity of PVA-MS/PCDMs increased with increasing PVA-MS pre-coated mass. The relative Zeta potential of the PVA-MS/PCDMs, which were measured using 0.01 mol· L^-1 KCl solution, pH 8.0 ±0.2 and at 20℃, reached a peak value of - 36.4 mV with pre-eoated mass of 15.7 g·m^-2 PVA-MS on the membranee surface, in addition, evolutions of PVA-MS/PCDMs flux versus time were investigated using a 4 hours short-term filtration experiment at 9.5 kPa in an SMBR and the permeability coefficient of PVA-MS/PCDMs were measured by the extracellular polymeric substances (EPS) diffusion experiments. Results indicated that the PVA-MS/PCDMs presented dramatically high anti-fouling characteristics when the pre-coated mass of PVA-MS was 23.9-61.9 g·m^-2 .
出处 《环境科学》 EI CAS CSCD 北大核心 2009年第7期1983-1989,共7页 Environmental Science
基金 教育部新世纪优秀人才支持计划项目(NCET-07-0141)
关键词 预涂动态膜 清水过滤阻力 亲水性 ZETA电位 抗污染性 pre- coated dynamic membrane pure water permeation resistance hydrophilicity Zeta potential anti-fouling characteristics
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  • 1Owen G, Bandi M, Howell J A, et al. Economic assessment of membrane processes for water and wastewater treatment [J]. J Memb Sci, 1995, 102: 77-91.
  • 2Noor M J M M, Ahmadun F R, Mohamed T A, et al. Performance of flexible membrane using kaolin dynamic membrane in treating domestic wastewater [J]. Desalination, 2002, 147(1-3): 263-268.
  • 3张捍民,乔森,叶茂盛,张兴文,杨凤林.预涂动态膜-生物反应器处理生活污水试验研究[J].环境科学学报,2005,25(2):249-253. 被引量:25
  • 4Cai B, Ye H, Yu L. Preparation and separation performance of a dynamically formed MnO2 membrane [J]. Desalination, 2000, 128 (3) : 247-256.
  • 5Altman M, Semiat R, Hasson D. Removal of organic foulants from feed waters by dynamic membranes [ J]. Desalination, 1999, 125( 1- 3) : 65-75.
  • 6任建新,张保成.膜技术和环境保护中的水处理(英文)[J].膜科学与技术,2001,21(1):25-29. 被引量:20
  • 7Hemandez Rojas M E, Van Kaam R, Schetrite S, et al. Role and variations of supematant compounds in submerged membrane bioreactor fouling [ J ]. Desalination, 2005, 179 (1-3) : 95-107.
  • 8Lee W, Kang S, Shin H. Sludge characteristics and their contribution to microfiltration in submerged membrane bioreaetors [J]. J Memb Sci, 2003, 216(1-2): 217-227.
  • 9李娜,刘忠洲,续曙光.耐污染膜——聚乙烯醇膜的研究进展[J].膜科学与技术,1999,19(3):1-7. 被引量:41
  • 10Wilen B M, Jin B, Lant P. The influence of key chemical constituents in activated sludge on surface and flocculating properties [J]. Wat Res, 2003, 37(9): 2127-2139.

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